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JPS641524B2 - - Google Patents
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JPS641524B2 - - Google Patents

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Publication number
JPS641524B2
JPS641524B2 JP54010070A JP1007079A JPS641524B2 JP S641524 B2 JPS641524 B2 JP S641524B2 JP 54010070 A JP54010070 A JP 54010070A JP 1007079 A JP1007079 A JP 1007079A JP S641524 B2 JPS641524 B2 JP S641524B2
Authority
JP
Japan
Prior art keywords
furnace
radiation
container
energy
image
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP54010070A
Other languages
Japanese (ja)
Other versions
JPS55104412A (en
Inventor
Kenzo Yonezawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP1007079A priority Critical patent/JPS55104412A/en
Publication of JPS55104412A publication Critical patent/JPS55104412A/en
Publication of JPS641524B2 publication Critical patent/JPS641524B2/ja
Granted legal-status Critical Current

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  • Analysing Materials By The Use Of Radiation (AREA)
  • Blast Furnaces (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は例えば製鉄工場の高炉(熔鉱炉)等に
適用して好適な状態変化監視装置に係り、特に外
部から直接観測できない高炉内部の複雑な物理的
および化学的状態変化を立体画像化して監視する
状態変化監視装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a state change monitoring device suitable for application to, for example, a blast furnace (molten ore furnace) in a steel factory. The present invention relates to a state change monitoring device that monitors state changes by converting them into stereoscopic images.

一般に、高炉における製銑作業にあつては、第
1図に示すようにコンベヤ1を用いてコークス、
鉱石をホツパ2aへ、石灰石をホツパ2bへ装入
した後、これらのホツパ2a,2bよりコーク
ス、鉱石および石灰石を交互に上ベル3および下
ベル4を介して炉内部5に装填し、この状態で下
部羽口6から送風機にて炉内部5に衝風を送入す
る。衝風は予め熱風炉7にて熱したものを用い
る。熱風炉7はある時間ガスを燃焼して炉内格子
積煉瓦8に蓄熱する。次に、送風機より冷風を送
つて熱交換し熱風とする。熱風は指定温度とする
ため一部冷風を混入する。この場合熱風の圧力お
よび流量は一定であることが望まれる。
Generally, during iron making work in a blast furnace, a conveyor 1 is used to collect coke and
After ore is charged into the hopper 2a and limestone is charged into the hopper 2b, coke, ore and limestone are alternately charged into the furnace interior 5 from these hoppers 2a and 2b via the upper bell 3 and lower bell 4. A blower blows blast air into the furnace interior 5 from the lower tuyere 6. The blast air used is one that has been heated in advance in a hot air stove 7. The hot air stove 7 burns gas for a certain period of time and stores heat in the grate bricks 8 inside the furnace. Next, a blower sends cold air to exchange heat and make hot air. A portion of the hot air is mixed with cold air to maintain the specified temperature. In this case, it is desirable that the pressure and flow rate of the hot air be constant.

ところで、炉内部5のコークスは燃焼してCO
又はCO2ガスとなり鉱石を熔かして酸化鉄を還元
すると同時に、また鉱石中のMn,Siその他の不
純物をも還元する。そして、Mn,Si等は分離し
た熔鉄中に、ある量の炭素とともに混入して銑鉄
としこれを炉床9に溜める。この熔銑が炉床9に
充分溜ると、出銑口10を開いて待機する熔銑運
搬車に注入した後、混銑炉又は流鋳機へ運搬す
る。
By the way, the coke inside the furnace 5 burns and produces CO
Or it becomes CO 2 gas, which melts the ore and reduces iron oxide, while also reducing Mn, Si, and other impurities in the ore. Then, Mn, Si, etc. are mixed into the separated molten iron along with a certain amount of carbon to form pig iron, which is stored in the hearth 9. When the molten pig iron is sufficiently accumulated in the hearth 9, the tap hole 10 is opened and the molten pig iron is poured into a waiting molten pig transport vehicle, and then transported to a mixed pig iron furnace or a caster.

一方、高炉は溶解作用の特性上炉頂から出るガ
スはなお多くの可燃性COガスやH2、炭水化物を
含んでおり、これは燃料および動力源として活用
される。11はガス捕集管、12は冷却盤、13
は出滓口である。
On the other hand, due to the characteristics of the blast furnace's melting action, the gas emitted from the top of the furnace still contains a large amount of flammable CO gas, H 2 , and carbohydrates, which are used as fuel and a power source. 11 is a gas collection pipe, 12 is a cooling plate, 13
is the slag outlet.

ところで、以上のような高炉の製銑作業では、
炉操業中に炉況不調となる諸因子がある。即ち、
炉内部5へ装填した装填物は、物理的および化学
的に非常に複雑な変化をし、例えば装填物の分布
と下降状態、送風機の適否に起因して発生する炉
内温度の高低、送風圧力の高低によつて起るガス
分布状態の変調などが入り乱れて影響する。
By the way, in the above-mentioned blast furnace ironmaking work,
There are various factors that can cause furnace conditions to deteriorate during furnace operation. That is,
The charge loaded into the furnace interior 5 undergoes very complex physical and chemical changes, such as the distribution and descending state of the charge, the temperature inside the furnace due to the suitability of the blower, and the blowing pressure. Modulations in the gas distribution state caused by the height of the air flow mix and influence.

しかし、炉内部5のこれらの物理的および化学
的状態変化を監視する手段は現在のところ存在し
ておらず、専ら炉表面の圧力、熱電対や放射温度
計などを利用して表面の温度などを計測監視する
にすぎなかつた。炉内部5の温度放射(熱輻射)
による光は炉表面に達する迄に吸収、散乱してし
まつて観測することができず、レーザ光も炉内部
を通過させることができない。
However, there is currently no means to monitor changes in these physical and chemical conditions inside the furnace 5, and the only way to monitor these physical and chemical state changes is to monitor the furnace surface pressure, surface temperature, etc. using thermocouples, radiation thermometers, etc. It was merely a matter of measuring and monitoring. Temperature radiation inside the furnace 5 (thermal radiation)
The light emitted by the furnace is absorbed and scattered before it reaches the furnace surface and cannot be observed, and laser light cannot pass through the inside of the furnace either.

そこで、従来は炉内部5の状態変化を推測する
こと、および炉況の不調を未然に察知して対処す
ることは技術者の技量と経験にたよるしか方法が
なかつた。
Therefore, in the past, the only way to estimate changes in the state inside the furnace 5 and to detect and deal with malfunctions in the furnace beforehand was to rely on the skill and experience of engineers.

本発明は上記実情にかんがみてなされたもので
あつて、炉内部の状況を乱すことなく炉内部のガ
ス分布、装填物の分布およびその下降状態等をエ
ネルギー透過現像を利用して連続的に監視可能に
し、さらに炉操業中の炉況不調を未然に察知して
操業の安定化を図る状態変化監視装置を提供する
ものである。
The present invention has been made in view of the above circumstances, and uses energy transmission development to continuously monitor the gas distribution inside the furnace, the distribution of the charge, its descending state, etc., without disturbing the internal situation of the furnace. The object of the present invention is to provide a state change monitoring device that enables the operation of the furnace and also detects malfunctions in the furnace during operation in order to stabilize the operation.

以下、本発明の一実施例について図面を参照し
て説明する。第2図において20は仮想する炉の
外形を示し、この炉20のある横断面部をはさん
で高速で例えば放射線を発生する放射線走査器2
1と放射線検出器群22を配置している。この放
射線走査器21は炉横断面を扇状に横切るように
放射線ビームを振り、透過後の放射線強度を放射
線検出器群22で検出する。従つて、一回の放射
線走査の終了により、放射線検出器群22には第
2図Bのような扇状横断面の1次元投影データが
得られる。同図Bのは放射線強度、θは検出角
度(走査角度)である。そして、この1次元投影
データを図示しない電子計算機等の記憶部に記憶
しデータ処理に用いる。
An embodiment of the present invention will be described below with reference to the drawings. In FIG. 2, reference numeral 20 indicates the outer shape of an imaginary furnace, and a radiation scanner 2 that generates radiation at high speed across a certain cross section of the furnace 20.
1 and a radiation detector group 22 are arranged. This radiation scanner 21 swings a radiation beam across the furnace cross section in a fan shape, and a radiation detector group 22 detects the radiation intensity after passing through the radiation beam. Therefore, upon completion of one radiation scan, one-dimensional projection data of a fan-shaped cross section as shown in FIG. 2B is obtained on the radiation detector group 22. In the same figure, B is the radiation intensity, and θ is the detection angle (scanning angle). This one-dimensional projection data is then stored in a storage unit such as a computer (not shown) and used for data processing.

次に、第3図は炉20をはさんで放射線走査器
21と放射線検出器群22とを配置する点は同じ
であるが、特に第3図では放射線走査器21を複
数個配置して放射線走査器群21′を構成すると
ともに、各々の放射線走査器21…は個々に放射
線ビームを扇状に放射し、これによつて放射線検
出器群22に多方向からの投影データを得るよう
にしている。但し、それぞれの放射線検出器はコ
リメータによつて1つの方向が規定されるか、或
いは同じ時刻に1つの検出器に2個所以上の方向
から放射線が入射しないように放射線走査を制御
しているものとする。
Next, FIG. 3 is the same in that a radiation scanner 21 and a radiation detector group 22 are arranged across the furnace 20, but in particular in FIG. Each radiation scanner 21 constitutes a scanner group 21', and each radiation scanner 21 individually emits a radiation beam in a fan shape, thereby allowing the radiation detector group 22 to obtain projection data from multiple directions. . However, each radiation detector has one direction defined by a collimator, or radiation scanning is controlled so that radiation does not enter one detector from more than one direction at the same time. shall be.

次に、以上のような装置を用いて高炉内部の変
化状態を知ることについて詳細に説明する。今、
放射線走査器21で走査して高炉内部20に入射
した放射線強度をI0、高炉透過後の放射線強度を
とし、かつ放射線が単一エネルギーであると仮
定すると、放射線強度は(1)式のようになる。
Next, a detailed explanation will be given of how the above-described apparatus is used to determine the state of change inside the blast furnace. now,
Assuming that the radiation intensity that entered the blast furnace interior 20 after scanning with the radiation scanner 21 is I 0 , and the radiation intensity after passing through the blast furnace is assumed to be of single energy, the radiation intensity is as shown in equation (1). become.

I=I0exp(− 〓i μi・Δxi) ……(1) ここで、μiは放射線の通過径路に沿つた物質の
吸収係数であり、Δxiはその物質の径路に沿つた
長さに対応する値である。吸収係数μiは密度の関
数であつて物質によつて大きく異なる。また、放
射線のエネルギーによつて違つた値を示す。
I=I 0 exp (− 〓 i μ i・Δx i ) ...(1) Here, μ i is the absorption coefficient of the material along the radiation path, and Δx i is the absorption coefficient of the material along the path of the radiation. This is the value corresponding to the length. The absorption coefficient μ i is a function of density and varies greatly depending on the substance. It also shows different values depending on the energy of the radiation.

簡単のために、(1)式においてΔxi=Δx(一定)
とし、対数変換を行なうと、 ln(I0/I)=Δx・ 〓i Δμi ……(2) となる。右辺は吸収係数μiの和となる。即ち、(2)
式のような投影を多方向から短時間に求めて吸収
係数μiを連続的に復元する。これにより炉の横断
面の内部状態とその変化を知ることができる。吸
収係数μiの復元は放射線検出群22と電子計算機
とを結合することで行なわれる。
For simplicity, in equation (1), Δx i = Δx (constant)
Then, when logarithmic transformation is performed, ln(I 0 /I)=Δx・〓 i Δμ i ...(2). The right side is the sum of the absorption coefficients μ i . That is, (2)
The absorption coefficient μ i is continuously restored by obtaining projections as shown in the equation from multiple directions in a short time. This allows us to know the internal state of the cross section of the furnace and its changes. The absorption coefficient μ i is restored by combining the radiation detection group 22 and an electronic computer.

このように断面の画像再構成処理に電子計算機
を利用する方式は、コンピユータ断層撮影法、英
語ではComputed Tomography(以下、CTと指
称する)と呼ばれ、医療機器方面では頭部及び全
身の横断面撮像用に利用されている。これらの装
置は病変の位置を極めて明瞭に2次元像として描
出し、治療の方針決定に多大の効果を上げてい
る。CTの特徴はその高い密度分解能にある。即
ち、CTは液体、空気および固体等を区別できる
のは勿論のこと、放射線吸収係数が僅かしか異な
らない物体を識別分離できる。
This method of using a computer to reconstruct cross-sectional images is called computerized tomography (Computed Tomography (hereinafter referred to as CT) in English), and is used in medical equipment to perform cross-sectional cross-sectional imaging of the head and whole body. It is used for imaging. These devices depict the location of a lesion very clearly as a two-dimensional image, and are highly effective in determining treatment strategies. CT is characterized by its high density resolution. That is, CT can of course distinguish between liquids, air, solids, etc., and can also identify and separate objects whose radiation absorption coefficients differ only slightly.

従つて、本装置は放射線走査器21(又は放射
線検出群21′)と放射線検出器群22とを高炉
の炉床9から炉頂まで第4図のように複数段対向
配置することにより、炉内部の物理的および化学
的な状態変化を炉全体にわたつて時間的に連続し
て画像として再構成できる。従つて、状態変化監
視装置では、コークス、鉱石および石灰石等の装
填物についてその分布状態や下降状態を時々刻々
監視できる。装填物の降下速度の異常監視は炉計
装において重要なものの1つである。最も多く見
られる異常は、「たなつり」(炉内装填物が下降し
なくなること)と呼ばれる現象であつて大形高炉
に高温送風をした時に起りやすい。この場合に
は、炉内下部の圧力を下げる意味で送風流量を減
ずればたなは下がる。
Therefore, this device can detect the blast furnace by arranging the radiation scanner 21 (or the radiation detection group 21') and the radiation detector group 22 in multiple stages facing each other from the hearth 9 to the top of the blast furnace as shown in FIG. Changes in internal physical and chemical conditions can be reconstructed as images continuously over time throughout the reactor. Therefore, the state change monitoring device can constantly monitor the distribution and descending state of charges such as coke, ore, and limestone. Abnormal monitoring of the rate of descent of the charge is one of the important aspects of furnace instrumentation. The most common abnormality is a phenomenon called ``tanatsuri'' (the filling in the furnace no longer descends), which tends to occur when high-temperature air is blown into large blast furnaces. In this case, the cane will be lowered by reducing the air flow rate to lower the pressure in the lower part of the furnace.

また、この装置では、同様の原理に基づき送風
圧力の高低によつて起るガス分布状態の変化も把
握できる。
Furthermore, with this device, based on the same principle, it is also possible to grasp changes in the gas distribution state caused by changes in the blowing pressure.

ところで、(2)式は以下のような式に置き換える
ことができる。
By the way, equation (2) can be replaced with the following equation.

lo(I0/I)=Δx 〓i μi/ρi・ρi ……(3) ここで、ρiは放射線の通過経路に沿つた物質の
密度である。またμi/ρiは物質の質量吸収係数と
いい、これは既に知られているように同じエネル
ギーの放射線に対しては、鉛のように大きい原子
番号を持つたものを除外すれば、殆んどすべての
物質についてほぼ一定の値である。そこで、μi
ρi=αとすれば、(3)式は Io(I0/I)=Δx・α 〓i ρi ……(4) とすることができる。この式の右辺は物質の密度
の和である。この場合も前述同様、(4)式に基づく
投影を多方向から短時間で行なうことにより、物
質の密度ρiを連続的に復元できる。
l o (I 0 /I) = Δx 〓 i μ ii・ρ i ...(3) Here, ρ i is the density of the material along the radiation path. Also, μ ii is called the mass absorption coefficient of a substance, and as is already known, for radiation of the same energy, if you exclude substances with large atomic numbers such as lead, most of the The value is almost constant for all substances. Therefore, μ i /
If ρ i =α, equation (3) can be changed to I o (I 0 /I)=Δx·α 〓 i ρ i ……(4). The right side of this equation is the sum of the densities of the materials. In this case, as described above, the density ρ i of the substance can be continuously restored by performing projections based on equation (4) from multiple directions in a short time.

ρiを正確に求める場合には次のような手段も考
えられる。先ず、(2)式よりμiを求めその値からそ
の点の物質が何であるか判定する。通常、高炉内
部の装填物は限られているためである。よつて、
その物質の質量吸収係数μi/ρiは実験値等から分
るので、新ためて(3)式に代入して求めれば、(4)式
より正確なρiを求めることができる。従つて、以
上のような構成のものでは、高炉内の密度分布及
び変化を立体的に連続的に観察できるだけでな
く、固体、液体あるいは気体の温度による密度変
化を可視化して高炉内の温度分布を求めることも
できる。
In order to accurately obtain ρ i , the following methods can also be considered. First, calculate μ i from equation (2), and use that value to determine what kind of substance is present at that point. This is because the charge inside the blast furnace is usually limited. Then,
Since the mass absorption coefficient μ ii of the substance is known from experimental values, etc., by substituting it into equation (3) and finding it again, it is possible to find ρ i more accurately than equation (4). Therefore, with the above configuration, not only can the density distribution and changes in the blast furnace be observed continuously in three dimensions, but also the temperature distribution in the blast furnace can be visualized by visualizing the density changes due to temperature of solids, liquids, or gases. You can also ask for

以上詳記したように本発明装置によれば、装填
物を装填する容器をはさんでエネルギーの発生器
と検出器群を複数段対向配置し、放射線エネルギ
ーの透過現象および電子計算機を利用して容器内
部の装填物の物理的および化学的変化を投影する
構成にしたので、容器内部の状態を乱すことなく
装填物の分布およびその下降状態、さらに容器内
部の温度分布およびガス分布状態を連続的に投影
して監視できる。従つて、本装置は従来のように
技術者の技量や経験によることなく、投影データ
から例えば高炉操業中の炉況不調を未然に察知す
ることができ、さらに自動制御技術とあいまつて
操業を飛躍的に安定化することができる。
As described in detail above, according to the present invention, the energy generator and the detector group are arranged in multiple stages facing each other across the container into which the charge is loaded, and the radiation energy transmission phenomenon and the electronic computer are utilized. Since the structure is designed to project the physical and chemical changes of the charge inside the container, it is possible to continuously monitor the distribution of the charge and its descending state, as well as the temperature distribution and gas distribution state inside the container, without disturbing the conditions inside the container. can be projected and monitored. Therefore, this device can detect, for example, malfunctions in the furnace during blast furnace operation from projection data, without relying on the skills and experience of engineers like in the past, and when combined with automatic control technology, it can dramatically improve operations. can be stabilized.

また、炉内の状態を時々刻々撮像するので、炉
内装填物の物理的、化学的変化のメカニズムや操
業中の炉況不調となる諸因子等を的確に究明でき
る。
In addition, since the state inside the furnace is imaged every moment, it is possible to accurately investigate the mechanism of physical and chemical changes in the contents inside the furnace and various factors that cause poor furnace conditions during operation.

なお、本装置の適用は高炉のみに限らないこと
は言うまでもない。要は機器の内部が高温等で物
理的、化学的にすこぶる複雑な変化をなし外部か
らそれを直接観測できない場合に広く適用できる
ものである。
It goes without saying that the application of this device is not limited to blast furnaces. In short, it can be widely applied to cases where the inside of a device undergoes extremely complex physical and chemical changes due to high temperatures, etc., and these changes cannot be directly observed from the outside.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の高炉本体の一般的構造を示す断
面図、第2図は本発明に係る状態変化監視装置の
基本構成を示す図であつて同図Aは放射線走査器
および放射線検出器群との関係を示す図、同図B
は放射線検出器群で検出した放射線強度を意味す
る1次元投影データの図、第3図は本発明装置の
他の例を説明する図、第4図は本発明装置の具体
例として高炉に適用した場合の断面図である。 5……炉内部、9……炉床、20……高炉、2
1……放射線走査器(放射線発生器)、21′……
放射線走査器群、22……放射線検出器群。
FIG. 1 is a cross-sectional view showing the general structure of a conventional blast furnace main body, and FIG. 2 is a view showing the basic configuration of a state change monitoring device according to the present invention. A diagram showing the relationship between
is a diagram of one-dimensional projection data indicating the radiation intensity detected by a group of radiation detectors, Figure 3 is a diagram explaining another example of the device of the present invention, and Figure 4 is a specific example of the device of the present invention applied to a blast furnace. FIG. 5... Furnace interior, 9... Hearth, 20... Blast furnace, 2
1...Radiation scanner (radiation generator), 21'...
Radiation scanner group, 22... Radiation detector group.

Claims (1)

【特許請求の範囲】[Claims] 1 装填物が容器内部の高温により化学的および
物理的な状態変化を呈するものにおいて、その容
器の一方外周に該容器内部の装填物内を充分に透
過するだけの放射線等のエネルギーを発生する少
なくとも一個のエネルギー発生器を設け、また前
記容器の他方外周に前記エネルギー発生器から発
生するエネルギーを検出する検出器群を配置する
とともに、これらエネルギー発生器および検出器
群を前記容器の縦方向に複数段にわたつて配置
し、前記エネルギー発生器から容器内部を通つて
検出器群で検出されたエネルギーを電子計算機で
画像再構成処理を行つて断面像を得るとともに炉
各段の検出器群からの断面像から炉内部の立体像
を作成し、この立体像を表示して炉内部における
装填物の物理的・化学的状態の変化を監視し、か
つ、炉況不調を未然に察知するようにしたことを
特徴とする状態変化監視装置。
1. In cases where the loaded material undergoes chemical and physical state changes due to the high temperature inside the container, at least one part of the outer periphery of the container that generates enough energy such as radiation to pass through the loaded material inside the container. One energy generator is provided, and a group of detectors for detecting the energy generated from the energy generator is arranged on the other outer periphery of the container, and a plurality of energy generators and detector groups are arranged in the longitudinal direction of the container. The energy transmitted from the energy generator through the inside of the vessel and detected by the detector group is processed by an electronic computer to reconstruct the image to obtain a cross-sectional image. A 3D image of the inside of the furnace was created from the cross-sectional image, and this 3D image was displayed to monitor changes in the physical and chemical state of the charges inside the furnace, and to detect malfunctions in the furnace before they occurred. A state change monitoring device characterized by:
JP1007079A 1979-01-31 1979-01-31 State change supervisory apparatus Granted JPS55104412A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1007079A JPS55104412A (en) 1979-01-31 1979-01-31 State change supervisory apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1007079A JPS55104412A (en) 1979-01-31 1979-01-31 State change supervisory apparatus

Publications (2)

Publication Number Publication Date
JPS55104412A JPS55104412A (en) 1980-08-09
JPS641524B2 true JPS641524B2 (en) 1989-01-11

Family

ID=11740107

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1007079A Granted JPS55104412A (en) 1979-01-31 1979-01-31 State change supervisory apparatus

Country Status (1)

Country Link
JP (1) JPS55104412A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4897406U (en) * 1972-02-22 1973-11-19

Also Published As

Publication number Publication date
JPS55104412A (en) 1980-08-09

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